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    • 4. 发明专利
    • GENERATION AND SEA WATER DESALTING COMBINED DEVICE
    • JPH1047015A
    • 1998-02-17
    • JP22440296
    • 1996-08-07
    • TOKYO GAS ENG KKCHIYODA CHEM ENG CONSTRUCT CO
    • YOSHIDA TAKEJIFUJIOKA HIROSHINISHIZAWA HIROSHIOYAMADA AKIRA
    • F01K9/00F01K17/04
    • PROBLEM TO BE SOLVED: To provide a generation and sea water desalting combined device to ensure a constant generating amount regardless of a fluctuation in a fresh water amount and provide high integral heat energy efficiency for generation and fresh water generation, and high economical efficiency. SOLUTION: A generation and sea water desalting combined device comprises a circulation fluidized bed boiler 16 to generate superheated steam by burning fuel, such as RDF; a back pressure bleed steam turbine 18 to introduce steam from a boiler and convert it into a power to drive a generator 17; a multiple effect vaporizing can device 34 to desalt sea water by means of back pressure steam of a turbine serving as a heat source; an auxiliary condenser 22 to condense surplus back pressure steam; and deaerator 28 to deaerate condensate from a vaporizing can device for a multiple effect and condensate from a condenser by middle pressure steam bled and feed it to a boiler. This constitution realizes a system having extremely high thermal efficiency. Further, thermal power generating equipment is provided with an auxiliary condenser to condense surplus back pressure steam flowing out from a back pressure steam turbine, whereby generation by a constant output is practicable regardless of a fluctuation in a fresh water amount of a sea water desalting device.
    • 6. 发明专利
    • QUALITY CONTROL IN HEAT QUANTITY CONTROLLER
    • JPH0375409A
    • 1991-03-29
    • JP21246389
    • 1989-08-18
    • TOKYO GAS CO LTDTOKYO GAS ENG KK
    • NUKUI KAZUMITSUOHASHI TOSHIOARAI MASAHIKOYAMAMOTO YOSHIHIRO
    • F23N1/00B01F15/04F23K5/00
    • PURPOSE:To make it possible to carry out respective flow rate control for a fluid for dilution and a fluid for increasing heat with both fluids mutually related by setting a value that is the addition of the operational output of a heat quantity controller and the value of flow rate that is derived from a balance formula for heat quantities in mixing to a flow rate controller which constitutes a flow rate control loop for the fluid for increasing heat. CONSTITUTION:A calculator 11b derives the value of flow rate of a fluid for dilution from a balance formula of Wobbe index in the mixing of a fluid for receiving heat, fluid for dilution, and fluid for increasing heat. The constitution is that this value is set in a flow rate controller 8b and at the same time a calculator 11c derives the value of flow rate for the fluid for increasing heat from a balancing formula of the quantities of heat in mixing. Further, the calculation to add the operational output of a heat quantity controller 6 to this flow rate value is carried out and the value of the calculation is set to a flow rate controller 8c. With this arrangement, when the flow rate of the fluid the heat quantity of which is controller the heat quantity vary, it is pos sible to control respective flow rates with the fluid for dilution and the fluid for increasing heat mutually related.
    • 9. 发明专利
    • VENT SWITCHING VALVE UNIT FOR REGENERATIVE BURNER
    • JPH10132227A
    • 1998-05-22
    • JP28355396
    • 1996-10-25
    • SHINKO SHOJI CO LTDTOKYO GAS ENG KKNORTH AMERICAN MFG CO
    • DENNIS QUIN
    • F16K25/00F23D14/66F23L15/02
    • PROBLEM TO BE SOLVED: To cool members such as a valve disc or casing and to improve heat resistance by forming a vent part at an upstream side of the disc to close an air supply side at the time of exhausting, and supplying a small amount of the air from a vent part via a periphery of the disc even at the time of closing it. SOLUTION: When a valve disc 7 is forwarded to be brought into contact with a valve seat 6 at the time of burning the regenerative burner 4, a valve part of an exhaust passage 2 is closed, and the valve part of an air supply passage 1 is opened. Accordingly, the air from an upstream side of the passage 1 is supplied from a passage 3 to the burner 4 via a valve seat 5 for burning. The exhaust gas fed via the burner 4 is exhausted from the passage 3 at the passage 3 via the seat 6 by suction of an exhaust blower. In this case, ambient temperature air of the passage 1 is fed from a vent hole 11 of a plate 10 to a gap 12 between the hole 11 and a valve disc 7 by suction of suction of an exhaust blower, fed via a periphery of the disc 7, and exhausted via the passage 2 together with exhaust gas. At this time, the ambient temperature air fed from the passage 1 cools the disc 7 and the casing.